US6566124B1ExpiredUtility
Processes for synthesis and purification of nondigestible fats
Est. expiryMar 23, 2018(expired)· nominal 20-yr term from priority
C12P 7/6418C12P 7/6436C12P 7/6454C12P 7/6458
69
PatentIndex Score
13
Cited by
49
References
23
Claims
Abstract
A process for removing digestible fat from a crude reaction mixture comprising nondigestible fat and at least one digestible fat selected from the group consisting of digestible fats having fatty acid chains, comprising the steps of: (1) treating the crude reaction mixture with an aqueous solution comprising lipase at a pH sufficient to obtain soaps from the fatty acid chains; and (2) removing the soaps.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1. A process for removing digestible fat from a crude reaction mixture comprising nondigestible fat and at least one digestible fat selected from the group consisting of digestible fats having fatty acid chains, comprising the steps of:
(1) treating the crude reaction mixture with an aqueous solution comprising lipase at a pH sufficient to form soaps from the fatty acid chains; and
(2) removing the soaps;
wherein the nondigestible fat comprises polyol fatty acid polyesters; and
wherein the digestible fat is selected from the group consisting of monoglycerides, diglycerides, triglycerides, alkyl esters, insufficiently esterified polyol polyesters and mixtures thereof.
2. A process according to claim 1 further comprising the step of adding surfactant and salt to the aqueous solution.
3. A process according to claim 2 , wherein the salt is selected from the group selected from the group consisting of alkali metal salts, alkaline earth metal salts and mixtures thereof.
4. A process according to claim 3 , wherein the salt is a calcium salt and wherein step (2) comprises precipitating and filtering out the soaps.
5. A process according to claim 2 , wherein the surfactant is selected from the group consisting of alkali metal soaps, alkaline earth metal soaps, sucrose monoesters, sucrose diesters, and mixtures thereof.
6. A process according to claim 1 , wherein the aqueous solution has a pH of from about 7 to about 10.
7. A process according to claim 2 , comprising the steps of:
(1) treating the crude reaction mixture with an aqueous solution comprising lipase, surfactant and salt to form an aqueous mixture;
(2) adjusting the pH of the aqueous mixture to from about 9 to about 10 at least once during step (1).
8. A process according to claim 7 , wherein the pH of the aqueous method is adjusted continuously.
9. A process according to claim 1 , wherein the lipase is present at a level of from about 0.01% to about 1%, by weight of the solution.
10. A process according to claim 1 , wherein the lipase specifically hydrolyzes fatty acid ester linkages of triglyceride at positions 1 and 3.
11. A A process according to claim 1 , wherein the lipase nonspecifically hydrolyzes fatty acid ester linkages of triglyceride.
12. A process according to claim 1 , further comprising the step of water-washing the nondigestible fat after the crude reaction mixture has been treated with the aqueous solution comprising lipase.
13. A process according to claim 12 , wherein the digestible fat is selected from the group consisting of monoglycerides, diglycerides, triglycerides and mixtures thereof; and wherein the process comprises the step of:
(1) treating the crude reaction mixture with an aqueous solution comprising lipase, surfactant and salt to obtain glycerol and soaps; and
(2) removing the glycerol and soaps.
14. A process for synthesizing polyol fatty acid polyesters comprising the steps of:
(1) mixing ingredients comprising (a) unesterified first polyol having hydroxyl groups, (b) second polyol esterified with fatty acids, (c) basic catalyst, and (d) emulsifying agent to form a mixture of ingredients;
(2) reacting the mixture of ingredients at a temperature sufficient to obtain a crude reaction mixture comprising ingredients, reaction products and by-products;
(3) removing at least a portion of the by-products from the crude reaction mixture;
(4) further reacting the reaction products and ingredients from step (3) at a temperature and for a time sufficient to esterify at least about 50% of the hydroxyl groups of the first polyol; and
(5) treating the resulting product of step (4) with an aqueous solution comprising lipase at a pH sufficient to form soaps from the fatty acid chains of the esterified second polyol and by-products.
15. A process according to claim 14 , further comprising the step of adding surfactant and salt to the aqueous solution.
16. A process according to claim 14 , wherein step (4) proceeds for a time sufficient to esterify at feast about 75% of the hydroxyl groups of the first polyol.
17. A process according to claim 14 , wherein step (4) proceeds for a time sufficient to esterify at east about 95% of the hydroxyl groups of the first polyol.
18. A process for synthesizing polyol fatty acid polyesters comprising the steps of:
(1) mixing ingredients comprising (a) unesterified first polyol having hydroxyl groups, (b) second polyol esterified with fatty acids, (c) basic catalyst, and (d) emulsifying agent to form a mixture of ingredients;
(2) reacting the mixture of ingredients at a temperature sufficient to obtain a crude reaction mixture comprising ingredients, reaction products and by-products;
(3) removing at least a portion of the by-products from the crude reaction mixture;
(4) further reacting the reaction products and ingredients from step (3) at a temperature and for a time sufficient to esterify at least about 50% of the hydroxyl groups of the first polyol; and
(5) treating the resulting product of step (4) with an aqueous solution comprising lipase at a pH sufficient to form fatty acids from the fatty acid chains of the esterified second polyol and by-products.
19. A process according to claim 18 , wherein step (4) proceeds for a time sufficient to esterify at least about 75% of the hydroxyl groups of the first polyol.
20. A process according to claim 18 , wherein step (4) proceeds for a time sufficient to esterify at least about 95% of the hydroxyl groups of the first polyol.
21. A process according to claim 18 , wherein the unesterified first polyol comprises sucrose, the second polyol esterified with fatty acids comprises fatty acid triglyceride, and the by-products comprise glycerol.
22. A process according to claim 18 , wherein step (4) proceeds for a time sufficient to form sucrose polyester comprising about 70%, by weight of the sucrose polyester, sucrose octa-esters.
23. A process according to claim 21 , wherein the step of removing the fatty acids and glycerol comprises distilling to remove the acids and water-washing and centrifuging to remove the glycerol.Cited by (0)
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